Oklahoma department of environmental quality



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Table D-17

Facility ID

Facility

Base Elevation (m)

UTM (m)

Easting

Northing

13665

American Foundry Group

165

291620

3956280

9943

OG&E Muskogee Generating

154

292335

3959747

9987

Owens Brockway Glass Cntr

182

289175

3960751

10113

Sintertec Div Of BPI Inc

157

291741

3962143

8668

Boral Bricks Of Texas LP

182

282067

3951391

10242

Global Stone St Clair Inc

211

334047

3940559

18787

Calpine Corp

213

257093

3988582

9257

Grand River Dam Auth

191

294073

4007568


Receptors

For the NAAQS analyses, G-P used receptor spacing identical to the spacing for the significant impact analysis. For each pollutant, these receptors extended out to the SID. The SID for PM, NOx, and SO2 are 0.8, 4.5, and 5.25 km, respectively. If the maximum impact location is in an area with receptor spacing greater than 100 m, then G-P also performed a refined analysis with additional receptors spaced apart at 100 m intervals.


D.2.8 PSD CLASS II INCREMENT ANALYSIS

Purpose and Methodology

As discussed in the result section, preliminary modeling of the proposed project indicated a significant impact (i.e., maximum impact at or above the PSD significance levels) for NO2, SO2, and PM10. Therefore, PSD review requires G-P to perform a full air quality analysis to demonstrate compliance with the PSD Class II Increments. The Increment impact analysis predicts the maximum ambient air concentration due to all Mill sources and off-site sources within the screening areas that affect or consume increment. The total of these concentrations must be less than the PSD Increment, as listed in Table D-18.


Table D-18

Pollutant

Averaging Time

Allowable PSD Increment (μg/m3)

Form of Standard

PM10

24-hour

30

High-second-highest for each year

Annual

17

Annual Mean

NO2

Annual

25

Annual Mean

SO2

3-hour

512

High-second-highest for each year

24-hour

91

High-second-highest for each year

Annual

20

Annual Mean



Inventory – G-P

In contrast to the NAAQS/AAQS analysis, the Increment inventory includes increases or decreases in actual emissions for non-major sources only after the minor source baseline date, and increases or decreases in emissions for major sources due to a change in the method of operation after the major source baseline date. Because the Mill is a major source, all emission increases after the major source baseline due to a change in the method of operation consume increment. The Mill was constructed after the major source baseline date for SO2 and PM10, 1975. Thus, the NAAQS inventory for PM10 and SO2 emissions from the Muskogee Mill are also the complete inventory of increment-affecting emissions from the Mill. Table D-13 above lists the NAAQS inventory emission rates for these pollutants.


In contrast, the PSD major source baseline date for NOX is March 1988. Table D-19 summarizes the NO2 emission calculations for increment-affecting emissions.
Table D-19



Model ID

Source Description

Source Modified Since 1988?

Emission Rates

Baseline

Maximum

Increment

(g/sec)

(g/sec)

(g/sec)

(lb/hr)

1112_8

PM 11 Yankee Wet End

No

0

0.5292

0.431

3.42

1112_7

PM 11 Yankee Dry End

No

0

0.5292

0.431

3.42

1112_20

PM12 Yankee

No

0

1.0584

0.718

5.70

13_13

Yankee Economizer

No

0

1.0584

0.783

6.21

14_13

Yankee Wet End

No

0

0.5292

0.433

3.43

14_17

Yankee Dry End

No

0

0.5292

0.433

3.43

15_13

Yankee Wet End

Yes

0

0.5292

0.529

4.2

15_18

Yankee Dry End

Yes

0

0.5292

0.529

4.2

PPRTO

Proposed RTO

No

0

0.063

0.063

0.5

Stack1

Boilers 1 and 2

No

31.67

46.620

14.750

118.68

Stack3

Boilers 3 and 4

No

67.95

98.255

30.305

240.51

Analysis Total




100.6

150.2

49.4

392.1

The inventory reflects the following conservative assumptions. Baseline emissions for all Yankee dryer emissions are set to zero. Actual emissions on the PSD baseline date were above zero for sources 11 through 14 as these sources existed in 1988. The analysis included the proposed RTO and did not include the credit from the shut-down of the existing RTO. PSD Baseline emissions for Stack 1 and Stack 3 sources reflect the average of 2002 and 2003 fuel usage. In 1988, all boilers were burning fuel oil. Emission factors for fuel oil are greater than natural gas emission factors. By assuming heat input for Boiler 1 (one of two boilers exhausting through Stack 1) was provided by gas instead of oil, the estimated baseline emissions are conservatively low, yielding a higher amount of emissions that affect increment.


Inventory – Competing Sources

A full analysis must include the emissions of competing sources. In contrast to the NAAQS analysis, the PSD Increment analysis includes emissions only from competing sources that affect increment. ODEQ identified several sources within 60 km of the Mill that consume increment. G-P modeled all PSD-consuming competing sources. Table D-20 presents modeling parameters of competing sources identified by ODEQ included in the analysis. As a conservative measure, the analysis used the potential emission rates for each pollutant affected by increment, regardless of source status during the baseline.


Receptors

For the PSD Increment analyses, G-P used receptor spacing identical to the spacing for the NAAQS analyses.



Table D-20
Facility / Source Description

Model ID

Increment Emissions (gram/sec)

Stack Ht

(m)

Stack Diam

(m)

Stack Temp

K

Exit Velocity

m/s

Volume Source Dimensions (m)

SO2

NO2

PM10

Sig y

Sig z

 































AMERICAN FOUNDRY GROUP

--

0

0

0













NA

NA


































OG&E































Unit #6

9946

828.58

0

26.71

152.4

6.6

402

25.2







Coal Crushing, Loading, and Handling

9947

0

0

0.068

10.0

NA

NA

NA

5

8.53


































OWENS BROCKWAY GLASS

--

0

0

0

NA

NA

NA

NA








































SINTERTEC DIV OF BPI INC































Kiln #1 (Shuttle)

10113

1.197

1.9908

0.315

10.1

0.4

505

19.1







Raw Mill

10117

0

0

0.214

10.1

0.4

294

19.1







Crushing

10118

0

0

0.214

10.1

0.4

294

19.1








































BORAL BRICKS OF TEXAS LP































Tunnel Kiln

8668

2.37

0

3.07

8.5

1.5

533

12.4








































GLOBAL STONE ST CLAIR INC































Rotary Lime Kiln #1 - KVS

10242

11.94

6.97

1.76

29.3

2.1

341

9.5







Rotary Lime Kiln #2 - Fuller

10243

20.41

11.91

2.82

30.5

2.1

341

14.4








































CALPINE CORP































Power Block 1, #1-1

18787

0.738

22.74

3.51

43.9

6.1

355

14.4







Power Block 2, #2-1

18789

0.738

22.74

3.51

43.9

6.1

355

14.4








































GRAND RIVER DAM AUTH































Electric Power Generation Unit #1

9257

775.78

0

64.65

153.9

6.1

408

27.6







Electric Power Generation Unit #2

9258

400.30

0

18.59

153.9

6.1

344

26.4








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